CN103318846B - Method for obtaining sulfur from sulfur compounds in coal chemical plant and electric power plant - Google Patents
Method for obtaining sulfur from sulfur compounds in coal chemical plant and electric power plant Download PDFInfo
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- CN103318846B CN103318846B CN201310246749.XA CN201310246749A CN103318846B CN 103318846 B CN103318846 B CN 103318846B CN 201310246749 A CN201310246749 A CN 201310246749A CN 103318846 B CN103318846 B CN 103318846B
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Abstract
The invention relates to a method for obtaining sulfur from sulfur compounds in a coal chemical plant and an electric power plant. The method comprises the following steps of: (1) dedusting exhaust gas from a coal burning boiler system, and then concentrating the exhaust gas to improve the content of sulfur dioxide in the exhaust gas; (2) heating the concentrated exhaust gas through an exhaust gas preheater, then introducing the exhaust gas into a constant temperature selective reduction reactor, and enabling the exhaust gas to react under the action of a selective reduction catalyst by adding hydrogen as a reducing agent so as to generate elemental sulfur, wherein the chemical equation is H2+SO2=S+H2O (1), and the heat generated by the reaction is taken away by a cooling coil which is arranged in the constant temperature selective reduction reactor to ensure that the temperature in the constant temperature selective reduction reactor is maintained at around 210-240 DEG C; (3) removing liquid sulfur from the exhaust gas subjected to catalytic reduction through a sulfur condenser, and introducing the exhaust gas into a Claus reaction device, wherein the liquid sulfur enters a liquid sulfur tank; and (4) burning the sulfur and sulfide contained in the tail gas passing through the Claus reaction device by using a combustion furnace so as to convert the sulfur and sulfide into sulfur dioxide, delivering the sulfur dioxide into the boiler system to mix with a dedusted process gas, and concentrating the mixture, wherein the gas discharged during concentration is mainly carbon dioxide.
Description
Technical field
The present invention relates to a kind of method extracting sulphur, particularly a kind of method obtaining sulphur from Coal Chemical Industry and power plant's sulfur compound.
Background technology
Coal Chemical Industry refers to coal to be that raw material changes into gas, liquid and solid through chemical process and is processed into the commercial run of a series of Chemicals further.The operation of coal chemical engineering equipment must rely on huge electric power energy consumption, thus in Coal Chemical Industry process of construction often enterprise need invest and establish power plant for self-supply.
In gasification hydrogasification process, element sulphur contained in coal and hydrogen generate hydrogen sulfide, gasification gas need could synthesize number of chemical product after desulfurization and decarburization, existing desulfurization and decarburization is a kind of method of physics, the such as technology such as low-temperature rectisol, NHD, MDEA absorption, hydrogen sulfide and carbonic acid gas dissolve in the solution under specified conditions (temperature, pressure etc.), under environment (temperature, pressure etc.) change, hydrogen sulfide flashes off, and this portion gas needs qualified discharge after treatment.
Power plant for self-supply adopts coal firing boiler generating, and the element sulphur contained in coal is oxidized to sulfurous gas in combustion.The technique of mainly " limestone-gypsum method " or " ammonia process of desulfurization " of the existing employing of the improvement for sulfurous gas, this technology uses extensively, but processing efficiency is not high, and regenerant is worth not high, can produce secondary pollution.
At present, coal chemical industry enterprises adopts two to overlap independently device process to two kinds of dusty gass that this produces, add the gross investment of project, the sulfur-bearing total amount of power plant is larger, cause reclaiming product economic worth lower, total emission volumn still keeps high-order, from environmental protection and recycling economy angle, does not well embody.
Summary of the invention
Technical problem to be solved by this invention is to overcome the defect existed in above-mentioned prior art, and provides a kind of method obtaining sulphur from Coal Chemical Industry and power plant's sulfur compound of the unified improvement of the sulfide of applicable coal chemical industry enterprises gasification and coal-fired boiler in power plant and recycling.
For solving the problems of the technologies described above, the method obtaining sulphur from Coal Chemical Industry and power plant's sulfur compound comprises the following steps:
(1) coal-burning boiler system flue gas out carries out concentration after carrying out dedusting, improves the content of sulfur dioxide in flue gas.
(2) flue gas through concentration enters constant temperature Chemoselective reduction device after smoke-gas preheater heating, and utilize additional hydrogen as reductive agent, under selective reduction catalyst effect, react generation elemental sulfur, and chemical equation is:
H
2+SO
2＝S+H
2O ①
React the heat produced to be taken away by the spiral coil cooling tube be arranged in described constant temperature Chemoselective reduction device, make temperature in described constant temperature Chemoselective reduction device maintain about 210-24O DEG C.
(3) after the flue gas of catalytic reduction deviates from molten sulfur by sulfur condenser, enter claus reaction device, wherein said molten sulfur enters molten sulfur pond.
(4) sulphur contained in the tail gas of claus reaction device and sulfide change into sulfurous gas after incinerator burns, deliver to boiler systems to mix with the Process Gas after dedusting, carry out concentration, the gas discharged in concentration process is mainly carbonic acid gas, component in former boiler smoke is mainly made up of carbonic acid gas and sulfurous gas, and the amount reducing carbonic acid gas makes sulfur dioxide concentration in gas assemble by concentration process.
In described step (3), enter the gasification sour gas also comprised through preheating of described claus reaction device, described sour gas enters described claus reaction device after acid gas separating tank carries out entering the heating of acid gas preheater after gas delivery.
Described claus reaction device comprises one-level claus reaction device, secondary claus reaction device, one-level sulfur condenser, secondary sulfur condenser and secondary reheater; Described firsts and seconds claus reaction device is in-built fills out high-efficiency activated catalyzer, first the described flue gas through catalytic reduction enters one-level claus reaction device and carries out catalyzed reaction, then one-level sulfur condenser is entered, the molten sulfur deviate from enters molten sulfur pond and flue gas enters secondary claus reaction device continuation catalyzed reaction, flue gas through quadric catalysis reaction enters secondary reheater and then enters secondary sulfur condenser, and the molten sulfur deviate from through condensation process enters molten sulfur pond.
The amount of reductive agent hydrogen is added by the H being arranged on claus reaction device in described step 2
2s/SO
21. ratio Analysis instrument determines according to reaction equation, namely enters the H of claus reaction apparatus
2s/SO
2ratio is as being greater than 2, then the amount reducing hydrogen makes H
2s/SO
2ratio trend towards 2; As being less than 2, then the amount increasing hydrogen makes H
2s/SO
2ratio trend towards 2.
Carry out the gas of concentration in described step 4 after deoxidation reactor deoxidation, react with the absorption cycle liquid of Trisodium Citrate in tail gas absorber:
SO
2(gas) → SO
2(liquid)
SO
2(liquid)+H
2o → H
++ HSO
3 -
Cit
3-+H
+→HCit
2 -
HCit
2-+H
+→H
2Cit
-
H
2Cit-+H
+→H
3Cit
3SO
2+3H
2O+Na
3Cit→3NaHSO
3+H
3Cit
Be mainly carbonic acid gas by above reaction end gas absorption tower expellant gas and reach effluent standard.
The method obtaining sulphur from Coal Chemical Industry and power plant's sulfur compound provided by the invention changes the construction mode that treatment system is overlapped in boiler desulfurization system and gasification sulfur recovery two, substantial saving in investment, any sour gas concentration of hydrogen sulfide can be met, the load variations of sulfur dioxide in flue gas concentration, changing sulfur recovery Cross unit because of concentration of hydrogen sulfide change cannot drive phenomenon, sulphur recovery efficiency is high, can more than 99.9% be reached, highly purified sulphur can be obtained, produce huge recycling economy to be worth, avoid desulphurization system because of sulfur dioxide corrosion phenomenon, and waste gas is better than national standard discharge, really realize energy-saving and emission-reduction, waste water is not produced in treatment process, there is no secondary pollution, and floor space of the present invention is little, construction cost is cheap, run simple, convenient operation and management, working cost is low, steam is self-produced personal.In view of the needs of China's modernization construction, this invention has wide market outlook, and its release must bring good economic benefit and social benefit.
Accompanying drawing illustrates:
Fig. 1 is the method flow schematic diagram obtaining sulphur from Coal Chemical Industry and power plant's sulfur compound;
Fig. 2 is claus reaction apparatus structure schematic diagram.
Embodiment:
Below in conjunction with accompanying drawing, inventive embodiment is described in further detail.
Embodiment 1: as shown in Figure 1, the present invention includes following steps:
(1) coal-burning boiler system flue gas out enters concentrating unit 2 and carries out concentration after cleaning apparatus 1, improves the content of sulfur dioxide in flue gas.
(2) flue gas through concentration enters constant temperature Chemoselective reduction device 4 after smoke-gas preheater 3 heats, utilize additional hydrogen as reductive agent, under selective reduction catalyst effect, react generation elemental sulfur, and chemical equation is:
H
2+SO
2＝S+H
2O ①
The heat reacting the steam of the 2.1-2.6MPaG produced is taken away by the spiral coil cooling tube being arranged on described constant temperature Chemoselective reduction device 4, makes described constant temperature Chemoselective reduction device 4 temperature maintain about 230 DEG C.
(3) deviate from molten sulfur through the flue gas of catalytic reduction by sulfur condenser 5 and produce the steam of 0.3-0.5MPaG, then add after the steam of 3.82MPaG or middle pressure steam through one-level reheater 6 and enter claus reaction device 7, wherein said molten sulfur enters molten sulfur pond 8.
(4) sulphur contained in the tail gas of claus reaction device 7 and sulfide change into sulfurous gas after incinerator 9 burns, deliver to boiler systems to mix with the Process Gas after dedusting, carry out concentration, the gas discharged in concentration process is mainly carbonic acid gas, and produces steam or the middle pressure steam of 3.82MPaG.
Embodiment 2: difference from Example 1 is:
In described step (3), enter the gasification sour gas also comprised through preheating of described claus reaction device 7, described sour gas enters after acid gas preheater 11 heats and enters described claus reaction device 7 after acid gas separating tank 10 carries out gas delivery.
Embodiment 3: difference from Example 1 is:
Described claus reaction device 7 comprises one-level claus reaction device 12, secondary claus reaction device 13, one-level sulfur condenser 14, secondary sulfur condenser 15 and secondary reheater 16; Described one-level claus reaction device 12 and secondary claus reaction device 13 is in-built fills out high-efficiency activated catalyzer, first the described flue gas through catalytic reduction enters one-level claus reaction device 12 and carries out catalyzed reaction, then one-level sulfur condenser 14 is entered, the molten sulfur deviate from enters molten sulfur pond and flue gas enters secondary claus reaction device 13 continues catalyzed reaction, flue gas through quadric catalysis reaction enters secondary reheater 16 and then enters secondary sulfur condenser 15, and the molten sulfur deviate from through condensation process enters molten sulfur pond 8.
Embodiment 4: difference from Example 1 is:
The amount of reductive agent hydrogen is added by the H being arranged on claus reaction device 7 in described step 2
2s/SO
21. ratio Analysis instrument 17 determines according to reaction equation, and namely enter the H2S/SO2 ratio of claus reaction apparatus 7 as being greater than 2, then the amount reducing hydrogen makes H
2s/SO
2ratio trend towards 2; As being less than 2, then the amount increasing hydrogen makes H
2s/SO
2ratio trend towards 2.
Above embodiments of the invention have been described in detail, but described content being only preferred embodiment of the present invention, can not being considered to for limiting practical range of the present invention.All equalizations done according to the present patent application scope change and improve, and all should still belong within patent covering scope of the present invention.
Claims (3)
1. from Coal Chemical Industry and power plant's sulfur compound, obtain a method for sulphur, it is characterized in that comprising the following steps:
(1) coal-burning boiler system flue gas out carries out concentration after carrying out dedusting, improves the content of sulfur dioxide in flue gas;
(2) flue gas through concentration enters constant temperature Chemoselective reduction device after smoke-gas preheater heating, and utilize additional hydrogen as reductive agent, under selective reduction catalyst effect, react generation elemental sulfur, and chemical equation is:
H
2+SO
2＝S+H
2O ①
React the heat produced to be taken away by the spiral coil cooling tube be arranged in described constant temperature Chemoselective reduction device, make temperature in described constant temperature Chemoselective reduction device maintain 230-240 DEG C;
(3) after the flue gas of catalytic reduction deviates from molten sulfur by sulfur condenser, enter claus reaction device, wherein said molten sulfur enters molten sulfur pond;
(4) sulphur contained in the tail gas of claus reaction device and sulfide change into sulfurous gas after incinerator burns, deliver to boiler systems to mix with the Process Gas after dedusting, carry out concentrating and processing, the gas discharged in concentration process is mainly carbonic acid gas;
The amount of reductive agent hydrogen is added by the H being arranged on claus reaction device in described step (2)
2s/SO
21. ratio Analysis instrument determines according to reaction equation, namely enters the H of claus reaction device
2s/SO
2ratio is as being greater than 2, then the amount reducing hydrogen makes H
2s/SO
2ratio trend towards 2; As being less than 2, then the amount increasing hydrogen makes H
2s/SO
2ratio trend towards 2;
In described step (3), enter the gasification sour gas also comprised through preheating of described claus reaction device, described coalification gas sour gas enters described claus reaction device after acid gas separating tank carries out entering the heating of acid gas preheater after gas delivery.
2. according to the method obtaining sulphur from Coal Chemical Industry and power plant's sulfur compound described in claim 1, it is characterized in that: described claus reaction device comprises one-level claus reaction device, secondary claus reaction device, one-level sulfur condenser, secondary sulfur condenser and secondary reheater; Described one-level claus reaction device and described secondary claus reaction device is in-built fills out high-efficiency activated catalyzer, first the described flue gas through catalytic reduction enters one-level claus reaction device and carries out catalyzed reaction, then one-level sulfur condenser is entered, the molten sulfur deviate from enters molten sulfur pond and flue gas enters secondary claus reaction device continuation catalyzed reaction, flue gas through quadric catalysis reaction enters secondary reheater and then enters secondary sulfur condenser, and the molten sulfur deviate from through condensation process enters molten sulfur pond.
3. according to the method obtaining sulphur from Coal Chemical Industry and power plant's sulfur compound described in claim 1, it is characterized in that: carry out concentrating in described step (4) and the gas processed after deoxidation reactor deoxidation, react with the absorption cycle liquid of Trisodium Citrate in tail gas absorber:
SO
2(gas) → SO
2(liquid)
SO
2(liquid)+H
2o → H
++ HSO
3 -
Cit
3-+H
+→HCit
2 -
HCit
2-+H
+→H
2Cit
-
H
2Cit-+H
+→H
3Cit
3SO
2+3H
2O+Na
3Cit→3NaHSO
3+H
3Cit
Be mainly carbonic acid gas by above reaction end gas absorption tower expellant gas and reach effluent standard.
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|---|---|---|---|
| CN201310246749.XA CN103318846B (en) | 2013-06-21 | 2013-06-21 | Method for obtaining sulfur from sulfur compounds in coal chemical plant and electric power plant |
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|---|---|---|---|
| CN201310246749.XA CN103318846B (en) | 2013-06-21 | 2013-06-21 | Method for obtaining sulfur from sulfur compounds in coal chemical plant and electric power plant |
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| CN103318846B true CN103318846B (en) | 2015-01-14 |
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Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152138A (en) * | 2015-08-28 | 2015-12-16 | 北京矿冶研究总院 | Method for treating copper pyrometallurgical flue gas |
| CN107185462B (en) * | 2017-06-23 | 2021-04-06 | 中国科学院过程工程研究所 | Suitable for high SO2Fluidized bed reactor and process for producing S by reducing metallurgical flue gas |
| CN108970385B (en) * | 2018-09-19 | 2024-01-16 | 北京巨亚国际环境科技股份有限公司 | Integrated multifunctional biomass boiler desulfurization and denitrification equipment |
| CN109045995B (en) * | 2018-09-19 | 2021-02-12 | 北京巨亚国际环境科技股份有限公司 | Deep dry desulfurization and denitrification method for biomass boiler |
| CN110237680A (en) * | 2019-06-17 | 2019-09-17 | 中国华能集团有限公司 | A kind of temperature equalization system and technique of synthesis gas reduction sulfur dioxide |
| CN111470476A (en) * | 2020-03-31 | 2020-07-31 | 武汉国力通能源环保股份有限公司 | Method for recycling and recovering sulfur from regenerated sulfur-containing tail gas subjected to active coke dry method flue gas treatment |
| CN113548646A (en) * | 2020-04-24 | 2021-10-26 | 北京北大先锋科技有限公司 | Method and system for reducing sulfur dioxide and recovering sulfur by using steel mill tail gas |
| CN112875652B (en) * | 2021-05-06 | 2021-08-24 | 中国恩菲工程技术有限公司 | Containing SO2Method for preparing sulfur from flue gas |
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| EP0669854B1 (en) * | 1992-11-18 | 1997-06-11 | Akzo Nobel N.V. | Process for removing sulphur dioxide from a sulphur dioxide-containing gas stream |
| EP1090675A1 (en) * | 1999-09-30 | 2001-04-11 | Gastec N.V. | Process for the removal of sulphur compounds from gases |
| CN101717074A (en) * | 2009-08-07 | 2010-06-02 | 山东齐鲁石化工程有限公司 | Double selectivity efficient sulfur recovery device |
| CN101659400B (en) * | 2009-09-11 | 2011-02-16 | 山东迅达化工集团有限公司 | Catalyst combination process of sulfur recovering device |
| CN101693164A (en) * | 2009-10-30 | 2010-04-14 | 邵志辉 | Method for obtaining high-purity sulphur from Claus reactive tail-gases |
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